US4361682A - Process for preparing bimodal or multimodal polymers of conjugated dienes - Google Patents

Process for preparing bimodal or multimodal polymers of conjugated dienes Download PDF

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Publication number
US4361682A
US4361682A US06/251,977 US25197781A US4361682A US 4361682 A US4361682 A US 4361682A US 25197781 A US25197781 A US 25197781A US 4361682 A US4361682 A US 4361682A
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conjugated diene
bimodal
lithium
barium
strontium
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Christian Freppel
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Compagnie Generale des Etablissements Michelin SCA
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Compagnie Generale des Etablissements Michelin SCA
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    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F36/00—Homopolymers and copolymers of compounds having one or more unsaturated aliphatic radicals, at least one having two or more carbon-to-carbon double bonds
    • C08F36/02—Homopolymers and copolymers of compounds having one or more unsaturated aliphatic radicals, at least one having two or more carbon-to-carbon double bonds the radical having only two carbon-to-carbon double bonds
    • C08F36/04—Homopolymers and copolymers of compounds having one or more unsaturated aliphatic radicals, at least one having two or more carbon-to-carbon double bonds the radical having only two carbon-to-carbon double bonds conjugated

Definitions

  • the object of the present invention is a process which makes it possible to modify the molecular weight distribution upon the synthesis of a homopolymer of a conjugated diene or a copolymer of a conjugated diene with another conjugated diene or with a vinyl aromatic compound.
  • the object of the present invention is to remedy these drawbacks by providing a process which is economically more interesting and which makes it possible easily to modify and regulate the molecular weight distribution during the course of the synthesis of a homopolymer of a conjugated diene or a copolymer of a conjugated diene with another conjugated diene or with a vinyl aromatic compound and to obtain a bimodal or multimodal homopolymer or copolymer.
  • the applicant has unexpectedly found that it is possible to achieve this purpose when the homopolymerization of the conjugated diene or the copolymerization of the conjugated diene with another conjugated diene or with a vinyl aromatic compound by the use of the catalyst systems described above is effected in the presence of a modifying agent which is not a polymerization initiator.
  • the present invention concerns a process of preparing a homopolymer of a conjugated diene or a copolymer of a conjugated diene with another conjugated diene or with a vinyl aromatic compound, whether bimodal or multimodal, which consists in polymerizing the monomer(s) in a reacting medium at a temperature of between 20° C. and 200° C. in the presence of a catalyst system comprising an organolithium initiator, a barium, strontium or calcium compound, and an organometallic compound of a metal of group 2B or 3A of the periodic classification of elements of the Mendeleev Table, characterized by adding hydrogen as a modifying agent to the reaction medium during the course of the polymerization reaction.
  • This process makes is possible to modify the molecular weight distribution as desired and to obtain improved properties of raw tackiness, raw coherence and machineability without requiring additional amounts of catalyst and without, at the same time, penalizing the other properties.
  • the process of the invention makes is possible to obtain homopolymers and copolymers having bimodal or multimodal molecular weight distributions.
  • the fraction or fractions obtained after addition of the modifying agent are of low molecular weight.
  • the average molecular weights of said fraction or fractions of low molecular weight as well as the quantity of these low molecular weights are a function of the amount of the modifying agent added and of the time when this modifying agent is added during the course of the polymerization reaction.
  • the amount to be added and the time of the addition as a function of the percentage of conversion of the monomers at the time in question as compared with the final conversion percentage, it is possible to prepare bimodal or multimodal homopolymers and copolymers, the quantity of the high and low molecular weights of which as well as the respective average molecular weights of these high and low molecular weights can be regulated as desired.
  • the hydrogen is added during the course of the polymerization reaction and preferably when the conversion of the monomers is between 20% and 90%.
  • the polymerization process can be conducted in bulk or in solution in a hydrocarbon solvent either batchwise or continuously. In the latter case, one operates in two or more reactors placed in series at identical or different polymerization temperatures. Depending on the extent of the effect desired, the hydrogen is added in one or more portions.
  • organolithium initiator there is understood, first of all, any organometallic compound having one or more carbon-lithium bonds, secondly, any radical-ion adduct of lithium and of certain polynuclear aromatic hydrocarbons, thirdly, metallic lithium itself and, finally, the oligomers produced by the addition of lithium to conjugated dienes or substituted styrenes.
  • organolithium initiator As representative examples of organolithium initiator, the following compounds may be mentioned:
  • the aliphatic organolithiums such as ethyl lithium, n-butyl lithium, isobutyl lithium, sec-butyl lithium, tert.-butyl lithium, isopropyl lithium, n-amyl-lithium, isoamyl lithium; the alkenyl organolithiums such as allyl lithium, propenyl lithium, isobutenyl lithium, the "living" polybutadienyl lithium, polyisoprenyl lithium and polystyryl lithium polymers; the dilithium polymethylenes such as 1,4-dilithiobutane, 1,5-dilithiopentane, 1,20-dilithioeicosane; the aromatic organolithiums such as benzyl lithium, phenyl lithium and 1,1-diphenyl methyl lithium; the polylithiums resulting from the reaction of metallic lithium with aryl-substituted ethylene compounds such as 1,1-diphenylethylene, trans
  • a barium, strontium or calcium compound there are understood the hydrides BaH 2 , SrH 2 and CaH 2 , the mono- or polyfunctional organic acid salts of the formulas (R--COO) 2 Ba or Sr or Ca, R 1 --(COO) 2 Ba or Sr or Ca in which R and R 1 are organic radicals, the first monovalent and the second divalent, having no other functions capable of inactivating the organolithium initiator, and the corresponding thio acids, as well as the mono- or polyfunctional alcoholates and the corresponding thiolates; the mono- or polyfunctional phenates and the corresponding thiophenates; the salts of alcohol acids and phenol acids of barium, strontium or calcium such as the reaction products of barium, strontium or calcium with acetylacetone, dibenzoylmethane, thenoyltrifluoro acetone, benzoyltrifluoro acetone and benzoyl acetone; the organic derivatives of barium, stront
  • organometallic compounds of groups 2B and 3A there may be mentioned:
  • the zinc or cadmium dialkyls such as diethyl zinc, diethyl cadmium; the halogenated or nonhalogenated organoaluminums such as triethyl aluminum, triisobutyl aluminum, diethyl aluminum chloride, ethyl aluminum dichloride, ethyl aluminum sesquichloride, methyl aluminum sesquichloride; the dialkyl aluminum hydrides such as diethyl aluminum hydride, diisobutyl aluminum hydride, etc.
  • the barium, strontium or calcium compounds as well as the organometallic compounds of group 2B or 3A may be present in the form of a single compound having one of the following formulas:
  • M 1 represents barium, strontium or calcium
  • M 3 represents a metal of group 3A
  • M 2 represents a metal of group 2B of the periodic classification of elements of the Mendeleev Table
  • R 1 , R 2 , R 3 represent an alkyl or aralkyl radical
  • R 4 represents either an alkyl or aralkyl radical or a radical XB in which X represents an oxygen, sulfur or nitrogen atom and B is either an alkyl or aralkyl radical or a radical M 3 (R 5 R 6 ) in which R 5 , R 6 represent an alkyl or aralkyl radical.
  • the homopolymerization or copolymerization can also be carried out by means of the catalyst system defined above which furthermore contains an alkali metal alcoholate and more particularly an alcoholate having one of the following two formulas:
  • M' represents an alkali metal such as lithium, sodium or potassium and R represents an alkyl radical and n a whole number.
  • hydrocarbon solvent use may be made of aliphatic solvents, such as hexane and heptane, or aromatic solvents, such as benzene and toluene.
  • the process of the invention is suitable in particular for the homopolymerization of a conjugated diene or the copolymerization of a conjugated diene with another conjugated diene or with a vinyl aromatic compound.
  • conjugated dienes mention may be made of butadiene-1,3, isoprene, 2,3-dimethyl-butadiene-1,3, pentadiene-1,3, 2-methyl-pentadiene-1,3 and 2,4-hexadiene.
  • vinyl aromatic compounds there are suitable, in particular, styrene, ortho-, meta- and para-methylstyrene, "vinyl toluene", the di- and poly-methylstyrenes, p-tertiobutylstyrene, the vinyl naphthalenes, the methoxystyrenes, the halostyrenes, vinyl mesitylene and divinyl benzene.
  • the time elapsed between the start of the polymerization reaction and the moment when the modifying agent is added is designated in the example as “elapsed time” and the percentage of conversion reached at the time of the addition of the modifying agent is designated as “% conv.”.
  • FIGS. 1.1 and 1.2 of the drawing show the distribution of the molecular weights of the copolymers obtained at the end of the polymerization reaction which was obtained by gel permeation chromatography. The molecular weights are shown on the abscissa and the refraction index difference ⁇ i on the ordinate.
  • butyl lithium was then added in the order indicated.
  • the bottles were placed in a tank maintained thermostatically at 75° C. in which they were agitated.

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  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Polymerization Catalysts (AREA)
  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
  • Polymerisation Methods In General (AREA)
US06/251,977 1980-04-09 1981-04-06 Process for preparing bimodal or multimodal polymers of conjugated dienes Expired - Lifetime US4361682A (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
FR8008109A FR2480288A1 (fr) 1980-04-09 1980-04-09 Procede de preparation de polymeres de dienes conjugues ou de copolymeres conjugues soit entre eux, soit avec un compose vinylaromatique
FR8008109 1980-04-09

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US4361682A true US4361682A (en) 1982-11-30

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US (1) US4361682A (ja)
EP (1) EP0037617A1 (ja)
JP (1) JPS56157410A (ja)
AU (1) AU535395B2 (ja)
BR (1) BR8102168A (ja)
CA (1) CA1145883A (ja)
ES (1) ES8203094A1 (ja)
FR (1) FR2480288A1 (ja)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1285932A2 (en) * 2001-08-16 2003-02-26 The Goodyear Tire & Rubber Company Group 2 metal containing catalyst system
US6624267B1 (en) * 1999-01-06 2003-09-23 Michelin Recherche Et Technique S.A. Process of preparation of amino functionalized diene polymers, polymers of such type, rubber composition and tire casing containing those polymers
US20050061418A1 (en) * 2003-08-25 2005-03-24 Bates Kenneth Allen Pneumatic tire having a component containing high trans isoprene-butadiene rubber

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0877034A1 (en) * 1997-05-05 1998-11-11 The Goodyear Tire & Rubber Company Random trans SBR with low vinyl microstructure

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4079176A (en) * 1975-06-24 1978-03-14 Compagnie Generale Des Etablissements Michelin Polymerization process
US4080492A (en) * 1974-06-05 1978-03-21 Compagnie Generale Des Etablissements Michelin Butadiene polymerization process
US4129705A (en) * 1975-02-02 1978-12-12 Compagnie Generale Des Etablissements Michelin Polymerization process

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
NL120306C (ja) * 1955-07-29 1900-01-01
NL126912C (ja) * 1965-04-29
BE721676A (ja) * 1967-10-02 1969-04-01
FR2273822A1 (fr) * 1974-06-05 1976-01-02 Michelin & Cie Polymeres ou copolymeres a composition sterique modifiee, obtenus par mise en oeuvre d'une nouvelle composition catalytique
FR2340958A2 (fr) * 1974-06-05 1977-09-09 Michelin & Cie Procede de polymerisation ou de copolymerisation de dienes conjugues et polymeres ainsi obtenus

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4080492A (en) * 1974-06-05 1978-03-21 Compagnie Generale Des Etablissements Michelin Butadiene polymerization process
US4092268A (en) * 1974-06-05 1978-05-30 Compagnie Generale Des Etablissements Michelin, Raison Sociale Michelin & Cie Catalytic composition
US4129705A (en) * 1975-02-02 1978-12-12 Compagnie Generale Des Etablissements Michelin Polymerization process
US4079176A (en) * 1975-06-24 1978-03-14 Compagnie Generale Des Etablissements Michelin Polymerization process

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6624267B1 (en) * 1999-01-06 2003-09-23 Michelin Recherche Et Technique S.A. Process of preparation of amino functionalized diene polymers, polymers of such type, rubber composition and tire casing containing those polymers
US6800582B2 (en) 1999-01-06 2004-10-05 Michelin Recherche Et Technique S.A. Process of preparation of amino functionalized diene polymers, polymers of such type, rubber composition and tire casing containing those polymers
EP1285932A2 (en) * 2001-08-16 2003-02-26 The Goodyear Tire & Rubber Company Group 2 metal containing catalyst system
EP1285932A3 (en) * 2001-08-16 2003-04-02 The Goodyear Tire & Rubber Company Group 2 metal containing catalyst system
KR100929292B1 (ko) * 2001-08-16 2009-11-27 더 굿이어 타이어 앤드 러버 캄파니 높은 트란스 미세구조를 갖는 고무상 중합체의 합성방법
US20050061418A1 (en) * 2003-08-25 2005-03-24 Bates Kenneth Allen Pneumatic tire having a component containing high trans isoprene-butadiene rubber

Also Published As

Publication number Publication date
FR2480288B1 (ja) 1985-05-17
JPS56157410A (en) 1981-12-04
FR2480288A1 (fr) 1981-10-16
CA1145883A (en) 1983-05-03
ES501185A0 (es) 1982-02-16
AU535395B2 (en) 1984-03-15
BR8102168A (pt) 1981-10-13
AU6933281A (en) 1981-10-15
EP0037617A1 (fr) 1981-10-14
ES8203094A1 (es) 1982-02-16

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